GB849184A - Isomerisation of paraffin hydrocarbons - Google Patents
Isomerisation of paraffin hydrocarbonsInfo
- Publication number
- GB849184A GB849184A GB2813/59A GB281359A GB849184A GB 849184 A GB849184 A GB 849184A GB 2813/59 A GB2813/59 A GB 2813/59A GB 281359 A GB281359 A GB 281359A GB 849184 A GB849184 A GB 849184A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alumina
- catalyst
- mixture
- platinum
- per gram
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 229930195733 hydrocarbon Natural products 0.000 title abstract 3
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 3
- 238000006317 isomerization reaction Methods 0.000 title abstract 3
- 239000012188 paraffin wax Substances 0.000 title 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 17
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract 12
- 239000003054 catalyst Substances 0.000 abstract 9
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract 6
- 229910052697 platinum Inorganic materials 0.000 abstract 6
- 239000000203 mixture Substances 0.000 abstract 5
- 239000002245 particle Substances 0.000 abstract 5
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 abstract 4
- 238000005336 cracking Methods 0.000 abstract 4
- 230000000694 effects Effects 0.000 abstract 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 3
- 238000001354 calcination Methods 0.000 abstract 3
- 239000002131 composite material Substances 0.000 abstract 3
- 229910052739 hydrogen Inorganic materials 0.000 abstract 3
- 239000001257 hydrogen Substances 0.000 abstract 3
- 238000005470 impregnation Methods 0.000 abstract 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N methyl pentane Natural products CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 abstract 3
- 239000004215 Carbon black (E152) Substances 0.000 abstract 2
- 101710169849 Catalase isozyme A Proteins 0.000 abstract 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 2
- 159000000013 aluminium salts Chemical class 0.000 abstract 2
- 229910000329 aluminium sulfate Inorganic materials 0.000 abstract 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N anhydrous n-heptane Natural products CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 abstract 2
- 238000001035 drying Methods 0.000 abstract 2
- 239000000320 mechanical mixture Substances 0.000 abstract 2
- 238000002156 mixing Methods 0.000 abstract 2
- 239000000741 silica gel Substances 0.000 abstract 2
- 229910002027 silica gel Inorganic materials 0.000 abstract 2
- 229910000873 Beta-alumina solid electrolyte Inorganic materials 0.000 abstract 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 abstract 1
- 239000004115 Sodium Silicate Substances 0.000 abstract 1
- 239000002253 acid Substances 0.000 abstract 1
- 230000002378 acidificating effect Effects 0.000 abstract 1
- 150000003863 ammonium salts Chemical class 0.000 abstract 1
- 239000007864 aqueous solution Substances 0.000 abstract 1
- 238000000498 ball milling Methods 0.000 abstract 1
- 239000011230 binding agent Substances 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 239000004927 clay Substances 0.000 abstract 1
- 238000000354 decomposition reaction Methods 0.000 abstract 1
- 238000006356 dehydrogenation reaction Methods 0.000 abstract 1
- 239000000499 gel Substances 0.000 abstract 1
- 239000000017 hydrogel Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- KZNNRLXBDAAMDZ-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane trihydrate Chemical compound O.O.O.O=[Al]O[Al]=O KZNNRLXBDAAMDZ-UHFFFAOYSA-N 0.000 abstract 1
- 239000008188 pellet Substances 0.000 abstract 1
- 239000011148 porous material Substances 0.000 abstract 1
- 239000002244 precipitate Substances 0.000 abstract 1
- 230000001376 precipitating effect Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- 239000012266 salt solution Substances 0.000 abstract 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 abstract 1
- 229910052911 sodium silicate Inorganic materials 0.000 abstract 1
- 150000004684 trihydrates Chemical class 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2767—Changing the number of side-chains
- C07C5/277—Catalytic processes
- C07C5/2791—Catalytic processes with metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/12—Silica and alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/125—Halogens; Compounds thereof with scandium, yttrium, aluminium, gallium, indium or thallium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/19—Catalysts containing parts with different compositions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/04—Mixing
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The isomerisation of normal pentane, hexane or heptane is effected at 600 DEG -1,000 DEG F. and 50-1,000 p.s.i.g. using a LHSV of 0,5-40 in the presence of 0,5-20 moles of hydrogen per mole of hydrocarbon over a catalyst comprising a mechanical mixture of particles of size less than 100 microns diameter of (1) an alumina carrier having 0,05-5% by weight of platinum deposited thereon forming 0,1-0,9 of the weight of the mixture and (2) a silica-alumina cracking component having CAT-A cracking activity of 20-50 and preferably having an alumina content of at least 8%, the catalyst mixture being such that it has a dehydrogenating activity of 20-2,000, measured in units of 10-6 mols/second per gram of catalyst of benzene formed on passing cyclohexane over the catalyst at 750 DEG F. and 350 p.s.i.g. at a LHSV of 5,000 with hydrogen in a molar ratio to cyclohexane of 4 : 1.ALSO:A hydrocarbon isomerisation catalyst comprises a mechanical mixture of particles of less than 100 microns in diameter of (1) an alumina carrier having 0.05-5% of platinum deposited thereon and forming 0.1-0.9 of the weight of the mixture and (2) a silica-alumina cracking component having a CAT-A cracking activity of 20-50, the mixture being such that it has a dehydrogenation activity of 20-2,000 expressed as the rate of formation of benzene in 10-6 moles/second per gram of catalyst on passing cyclohexane over the catalyst at 750 DEG F. and 350 p.s.i.g. and a LHSV of 5,000 in the presence of 4 moles of hydrogen per mole of cyclohexane. The alumina supporting the platinum may have a surface area of 10-500 square metres per gram and may be a precipitate or gel. Although it may contain eta, chi, gamma, theta, delta or alpha alumina it is preferably ordinary activated alumina obtained by controlled calcination of alpha alumina trihydrate containing chi and gamma forms. It preferably has a density of 0.2-2 grams/c.c. Eta alumina obtained by calcining beta alumina trihydrate can also be used. The platinum may be deposited by impregnation with an aqueous solution of chloroplatinic acid or its ammonium salt followed by drying and reduction. The silica-alumina may be a natural clay or a synthetic composite. The latter may be formed by cogellation by mixing an acidic aluminium salt solution with sodium silicate, drying and calcining at 900-1400 DEG F. or by mixing separately formed hydrogels e.g. by ball-milling or by precipitating alumina on a previously formed silica gel or by impregnation of a preformed silica gel with an aqueous aluminium salt followed by decomposition. The composite may also be formed in spheroids as in U.S.A. Specification 2,384,946 or by the process of U.S.A. Specification 2,469,314 to give a product of pore diameter 50-75 , a surface area of at least 400 square metres per gram a particle density of 0.71-0.95 gram/c.c. and an alumina content of 18-38%. In general the composite should have a surface area of at least 300 square metres per gram, a particle density below 1.2 gram/c.c. and an alumina content of at least 8%. If it is desired to have the final catalyst mixture in pellet or other compounded form, this is preferably effected before impregnation of the alumina with platinum to avoid damaging the platinum during burning of the binder. The two components of the catalyst may have different particle size to assist in separating if necessary.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2813/59A GB849184A (en) | 1959-01-26 | 1959-01-26 | Isomerisation of paraffin hydrocarbons |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2813/59A GB849184A (en) | 1959-01-26 | 1959-01-26 | Isomerisation of paraffin hydrocarbons |
Publications (1)
Publication Number | Publication Date |
---|---|
GB849184A true GB849184A (en) | 1960-09-21 |
Family
ID=9746407
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2813/59A Expired GB849184A (en) | 1959-01-26 | 1959-01-26 | Isomerisation of paraffin hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB849184A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006010316A1 (en) * | 2004-07-29 | 2006-02-02 | China Petroleum & Chemical Corporation | A cracking catalyst for hydrocarbons and its preparation |
-
1959
- 1959-01-26 GB GB2813/59A patent/GB849184A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006010316A1 (en) * | 2004-07-29 | 2006-02-02 | China Petroleum & Chemical Corporation | A cracking catalyst for hydrocarbons and its preparation |
US9175230B2 (en) | 2004-07-29 | 2015-11-03 | China Petroleum & Chemical Corporation | Cracking catalyst and a process for preparing the same |
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